共聚反应的Monte Carlo模拟和竞聚率的概率估算

本文利用Monte Carlo方法模拟了二元共聚反应的链增长过程,并给出了估计竞聚率的概率统计处理。从统计观点上讲,这是一种在参数空间对每个栅格点计算后验概率密度的Bayesian统计,采用平滑函数对不规则的后验概率密度曲面(PPDS)进行平滑化,从而在置信的95尹。区域评价共聚反应竞聚率(r_1,r_2)。本方法用于计算苯乙烯-丙烯酸丁酯二元共聚反应时,所计算的竞聚率(r_(St),r_(BA))与文献结果甚为一致。     

带功能基的全氟烷基乙烯基醚的研究——3、四氟乙烯与-7,7-二氯-3-氧杂全氟庚烯-1的共聚反应及共聚物的转化

 研究了二个新的全氟烷基乙烯基醚7,7-二氯-3-氧杂全氟庚烯-1(M_0)和10,10-二氯-3,6-二氧杂全氟5-甲基癸烯-1(M₁)-与四氟乙烯(TFE)的共聚反应,聚合物的性质,并测定了TFE-M₀竞聚率。竞聚率的测定证明M₀较其它已报道的全氟烷基乙烯基醚的聚合活性都大。TFE-M₀共聚物通过化学反应可转化成相应的全氟羧酸甲酯树脂。     

价电子能级连接性指数及其应用

价电子能级连接性指数( ^fE)被定义为： ^fE=Σ(m_i·m_j…)^-0.5,m为价电子能级值。其中0、1阶指数公式分别为： ⁰E=Σ(m_i)^-0.5、 ¹E=Σ(m_i·m_j)^-0.5。 ⁰E、 ¹E与化合物的总键能(ΔE)、晶格能(U)、标准生成焓(Δ_fH^?_m)以及非金属氢化物的pKa呈现高度相关性。它们的线性回归方程为：ΔE=-48.0095+1402.9463¹E,r=0.9474, U=-328.0770+1541.9351 ¹E, r=0.9801,-Δ_fH^?_m=-266.9299+1324.6461 ¹E, r=0.9509, pKa=-20.9723+28.1756 ¹E, r=0.98884, pKa=-14.6102-7.835 ⁰E+40.6461 ¹E, R=0.9933。m、^fE具有物理意义明确、计算方法简单等优点,而且预测结果令人满意。     

丙烯酰胺与N,N′-亚甲基双丙烯酰胺的共聚反应研究

 本文利用凝胶模量测定法、气相色谱法和紫外光谱法对丙烯酰胺与N,N’-亚甲基双丙烯酰胺水溶液共聚反应进行了研究,证实了N,N’-亚甲基双丙烯酰胺的反应活性明显大于丙烯酰胺的反应活性。用气相色谱法测得单体的竞聚率分别为r_AM=0.117,,r_Bis=5.756;用紫外光谱法研究了聚合反应中氧化还原引发剂浓度和反应温度对聚合反应速率的影响,得出共聚反应速率方程中,氧化剂的方次为0.66,还原剂浓度的方次为0.55,并求出共聚反应表现活化能为37.1KJ/mol。     

N-异丙基丙烯酰胺温度敏感性水凝胶相转变动力学研究及其应用

 研究指出表观二级动力学方程可以很好地描述N-异丙基丙烯酰胺水凝胶的溶胀和消溶胀动力学.即溶胀动力学方程为dR/dt=k₁(R_e-R)²,消溶胀动力学方程为-dR/dt=k_c(R-R_e)².把这种水凝胶用于分离高分子水溶液时可引入“单位溶张比分离循环的合理时耗”这样一个参量.它根据溶胀和消溶胀过程中的起始溶胀比、平衡溶胀比、表观溶胀动力学常数和表观消溶胀动力学常数求出.具体公式为△t₁(T_s,T_c)=2/[R_c(T_s)-R₀(T_s)]²k_s(T_s)+15/[R₀(T_c)- R_s(T_c)]²k_c(T_c)^1/2在理想情况下,分离过程的“总合理时耗”与△t_1成正比,比例系数为分离过程中的除水总量与干凝胶用量的比值,即△t_r=W_W/WG·△t₁.当根据二个动力学方程求得的总时耗计算值处于(0.9△t_r,1.1△t_r)范围内时,表明所选干凝胶用量和循环溶胀比区段均合适.     

手性Salen Fe与2-乙基-4-甲基咪唑的分子识别研究

合成并表征了3个手性主体1 (t-Bu-Salen Fe^Ⅲ)、2 (unsym-Salen Fe^Ⅲ)和3 (Salen Fe^Ⅲ)，将其用于对客体4 (2-乙基-4-甲基咪唑，EMI) 逐级缔合反应的分子识别研究，首次测定了主体与EMI缔合反应逐级缔合常数K_Ⅰ、K_Ⅱ和反应过程热力学参数Δ_rG^?_m、Δ_rH^?_m、Δ_rS^?_m，详细地考察了主客体体系的圆二色(CD)光谱性质。实验表明：缔合常数K_Ⅰ和K_Ⅱ均按K(3)>K(2)>K(1)顺序递减，缔合反应是一放热、熵减过程，配位数的变化在UV-Vis电子吸收光谱和CD光谱上呈现出等吸收点位移，但没有改变缔合物双偶氮螯环的Δ构型。采用分子力学和量子化学相结合的方法，从理论上对实验结果作出了合理的解释。     

柚皮素、柚皮苷与溶菌酶相互作用的荧光光谱法研究

应用荧光光谱法研究了50%甲醇/水体系中柚皮素、柚皮苷与溶菌酶分子间的结合反应. 以Lineweaver-Burk双倒数方程和能量传递原理分别计算了两者与溶菌酶反应的结合常数(K)和结合距离(r): K_柚皮素^{25 ℃}＝4.00×10⁴, K_柚皮苷^{25 ℃}＝3.48×10⁴; r_柚皮素＝3.21 nm, r_柚皮苷＝3.30 nm, 以及由热力学参数的计算判断了两种分子与溶菌酶之间的作用力类型. 结果表明: 柚皮素、柚皮苷均能与溶菌酶以疏水作用相结合形成非共价化合物, 从而导致溶菌酶内在荧光的静态猝灭; 相对柚皮素, 柚皮苷与溶菌酶的结合距离增大, 作用强度减弱, 表明黄酮分子上多糖的取代不利于黄酮分子与蛋白之间的亲和作用. 根据Haslam等提出的多酚-蛋白质反应模型, 从分子水平初步探讨了糖取代对黄酮分子与蛋白相互作用减弱的原因.     

Ag(Ⅰ)、Pd(Ⅱ)异核金属簇合物的制备和晶体结构研究

The complexes of [Ag₂Pd₂(μ-dppm)₂(μ-S₂CNC₄H₈)₂(μ₃-S₂CNC₄H₈)₂](SbF₆)₂·Et₂O (1) and [AgPd(S₂CN C₄H₈)(μ-dppm)₂](SbF₆)·H₂O (2)were synthesized and their single crystal structures were determined by X-ray diffraction. The complex 1 is monoclinic system, space group P2₁/c with a=1.14370(3)nm, b=1.39025(4)nm, c=2.93579(8)nm, β=95.173(1)°, V=4.6490(2)nm³, Z=4, D_c=1.716g·cm^-3, μ(Mo Kα)=1682cm^-1, F(000)=2384, M_r=2401.98, R=0.0662, wR=0.1302. The complex 2 is monoclinic system, space group Cc with a=2.74136(6)nm, b=1.04317(2)nm, c=2.523990(10)nm, β=95.173(1)°, V=4.6490(2)nm³, Z=4, D_c=1.716g·cm^-3, μ(Mo Kα)=1682cm^-1, F(000)=2384, M_r=2401.98, R=0.0662, wR=0.1302. CCDC: 1, 213613; 2, 213612.     

X@(HAlNH)12和X(HAlNH)12 (X＝F－, Cl－, Br－, O2－, S2－, Se2－)复合物的结构和稳定性

用DFT的B3LYP方法在6-31G(d)基组的水平上, 对闭式多面体簇合物(HAlNH)₁₂及其内含式X@(HAlNH)₁₂和外接式X(HAlNH)₁₂ (X＝F^－, Cl^－, Br^－, O^2－, S^2－, Se^2－)复合物的结构进行了构型优化和能量计算, 并讨论了几何构型、自然键轨道(NBO)、振动频率、能量参数及NMR数据与结构的关系, 最后得到复合物结构的稳定性信息, 具有T_h对称性的X@(HAlNH)₁₂ (X＝F^－, Cl^－, Br^－, S^2－, Se^2－)复合物和具有C₃对称性的O^2－@(HAlNH)₁₂复合物为内含式的基态结构, 从能量角度分析, 内含式复合物比外接式复合物的结构稳定.     

三甲基胺氧化物希土配合物的振动光谱和配位结构研究

用三甲基胺氧化物(TMAO)与希土高氯酸盐和硝酸盐反应，制得了组成为：［Ln(TMAO)₆］(ClO₄)₃和［Ln(TMAO)₃(NO₃)］(NO₃)₂, (Ln=La、Nd、Sm、Gd)的配合物。用摩尔电导、IR、Raman光谱结合GF矩阵力常数及INDO分子轨道计算对其配位结构进行了研究。     

Monte Carlo estimation of kinetic parameters in polymerization reactions

A general method for estimating kinetic parameters in polymerization reactions using Monte Carlo simulation to represent the models of the reactions is developed. From a statistical point of view, the procedure is a Bayesian one in which a posterior probability density surface (PPDS) is calculated for points on a grid in the parameter space. A smoothing function is fitted to the PPDS, then a posterior probability region, which is similar to a confidence region, is calculated for the parameters. An application to a relatively trivial example, the Mayo–Lewis copolymerization model is shown in detail. Many other potential applications are suggested.     

N-vinylpyrrolidone and 4-vinyl Benzylchloride Copolymers: Synthesis,Characterization and Reactivity Ratios

The copolymers prepared in this study by free radical copolymerization of N-vinylpyrrolidone (M ₂) with 4-vinylbenzylchloride (M ₁) using 2,2′-azobisisobutyronotrile (AIBN) initiator in 1,4-dioxane solvent at 70°C were characterized by FTIR, ¹H-NMR and ¹³C-NMR techniques. Polymer solubility was tested in both polar and nonpolar solvents. The thermal properties were studied by thermogravimetric analysis (TGA) and differential scanning calorimeter (DSC). Copolymer compositions were established by H¹-NMR spectra, while reactivity ratios of the monomers were computed using the linearization methods viz., Fineman-Ross (FR) (r ₁ = 1.67 and r ₂ = 0.67), Kelen-Tudos (KT) (r ₁ = 1.77 and r ₂ = 0.65) and extended Kelen-Tudos (EK-T) (r ₁ = 1.72 and r ₂ = 0.63) methods at lower conversion. Furthermore, reactivity ratios in nonlinear error-in-variables method (RREVM) also compute the reactivity ratios (r ₁ = 1.76 and r ₂ = 0.66); these are found to be in good agreement with each other. The distribution of monomer sequence along the copolymer chain was calculated using a statistical method based on the calculated reactivity ratios.     

POLYACRYLONITRILE PRECURSORS FOR CARBON FIBER WITH IMIDOCARBOX YLIC ACID UNITS: COPOLYMERIZATION OF ACRYLONITRILE WITH MALEIMIDOBENZOIC ACID

ABSTRACT

4-Maleimidobenzoic acid (MBA) was explored as a comonomer in polyacrylonitrile (PAN) precursors for carbon fiber. The copolymerization of acrylonitrile (AN) with MBA was carried out in DMF. The reactivity of MBA was considerably less than that of AN, which was manifested as a negative reactivity ratio for the former. The r _MBA- values from ?0.24 to ?0.33 and r _AN values of 1.07 were obtained by Kelen-Tudos and extended Kelen-Tudos methods. The penultimate reactivity ratios were determined by both linear and non-linear methods. The values were r ₁=0.0093, r ₁′=0.0132, r ₂=1.063 and r ₂′=1.625. The relative MBA concentration in the copolymer decreased drastically on enhancing its content in the monomer mixture. The penultimate model could satisfactorily explain the feed-copolymer composition profile for the whole composition range. MBA caused a decrease in the apparent copolymerization rate and molecular weight in agreement with the observed trends in the reactivity ratios. A statistical prediction of monomer sequences based on reactivity ratios implied that MBA existed as a lone monomer unit between the long sequences of AN units. This sequence distribution is suited for the efficiency of MBA in cyclisation reaction, which stabilizes PAN during its pyrolysis. Optimum thermal stabilization effect and char yield were observed for copolymers with around 3 mol% MBA in the chain.     

EFFECT OF TEMPERATURE ON COPOLYMERIZATION PARAMETERS OF HYDROXYETHYL ACRYLATE AND METHYL METHACRYLATE

The copolymerization of 2-hydroxyethyl acrylate (HEA, M_1) and methylmethacrylate (MMA, M_2) in cyclohexanone was studied. The multiple experiments ofsolution copolymerization with low conversion were carried out at two sensitive compositionfeed points at 60, 80, 100, 120 and 140℃, respectively. The composition of the copolymerswas analyzed by ~1H-NMR. The reactivity ratios which were estimated by the Error-in-Variable Method (EVM) of Mayo-Lewis equation were found to be r_1 = 0.328, r_2 = 1.781for 60℃; 0.375, 1.709 for 80℃; 0.406, 1.654 for 100℃; 0.439, 1.540 for 120℃ and 0.455,1.400 for 140℃, and the 95% joint confidence intervals of the reactivity ratios were alsodetermined. According to r_1 and r_2, Arrhenius relations and the activity energy differencebetween the homo- and cross-propagation were calculated.     

Hydrophilic and hydrophobic copolymer systems based on acrylic derivatives of pyrrolidone and pyrrolidine

This article deals with the synthesis of hydrophilic methacrylic monomers derived from ethyl pyrrolidone [2‐ethyl‐(2‐pyrrolidone) methacrylate (EPM)] and ethyl pyrrolidine [2‐ethyl‐(2‐pyrrolidine) methacrylate (EPyM)] and their respective homopolymers. For the determination of their reactivity in radical copolymerization reactions, both monomers were copolymerized with methyl methacrylate (MMA), the reactivity ratios being calculated by the application of linear and nonlinear mathematical methods. EPM and MMA had ratios of r_EPM = 1.11 and r_MMA = 0.76, and this indicated that EPM with MMA had a higher reactivity in radical copolymerization processes than vinyl pyrrolidone (VP; r_VP = 0.005 and r_MMA = 4.7). EPyM and MMA had reactivity ratios of r_EPyM = 1.31 and r_MMA = 0.92, and this implied, as for the EPM–MMA copolymers, a tendency to form random or Bernoullian copolymers. The glass‐transition temperatures of the prepared copolymers were determined by differential scanning calorimetry (DSC) and were found to adjust to the Fox equation. Total‐conversion copolymers were prepared, and their behavior in aqueous media was found to be dependent on the copolymer composition. The swelling kinetics of the copolymers followed water transport mechanism case II, which is the most desirable kinetic behavior for a swelling controlled‐release material. Finally, the different states of water in the hydrogels—nonfreezing water, freezing bound water, and unbound freezing water—were determined by DSC and found to be dependent on the hydrophilic and hydrophobic units of the copolymers. © 2002 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 395–407, 2003     

Reactivity of acrylic monomers

Summary The copolymerization of N,N-diethylacrylamide (M_l) with methyl acrylate (M₂) was investigated and reactivity ratiosr ₁= 0.41 andr ₂ = 0.52 obtained. Also the distribution of diad fractions was calculated and the results were interpreted in terms of the product of reactivity ratios. The tendency of the two monomers to alternate was explained on the basis of differences in polatities between the double bonds, this explanation being supported both by the values ofe parameter and NMR spectroscopy data. A copolymerization mechanism was suggested.With 5 figures and 2 tables     

Effects of temperature on styrene–methacrylonitrile copolymerization

The free-radical copolymerization of styrene and methacrylonitrile was studied in toluene solution at 60, 90, and 120°C. Copolymer composition was estimated from gas-chromatographic measurement of unreacted monomer concentrations. Reactions were carried to about 20% conversion to minimize analytical errors. Reactivity ratios were calculated by using an integrated form of the Mayo-Lewis simple copolymerization equation. Reactivity ratios were not sensitive to reaction temperature. The values at 90°C are r₁ = 0.41 (methacrylonitrile) and r₂ = 0.37 (styrene). The r₁ values are higher than those reported by other workers, presumably because of advantages in the present analytical technique and calculation method. The negligible temperature dependence of reactivity ratios is in accord with theory. If monomer pairs exhibit pronounced dependence of reactivity ratios on polymerization temperature, this may indicate a change in mode of placement of units in the polymer chain.     

Radical‐initiated polymerization of β‐methyl‐α‐methylene‐γ‐butyrolactone

β‐Methyl‐α‐methylene‐γ‐butyrolactone (MMBL) was synthesized and then was polymerized in an N,N‐dimethylformamide (DMF) solution with 2,2‐azobisisobutyronitrile (AIBN) initiation. The homopolymer of MMBL was soluble in DMF and acetonitrile. MMBL was homopolymerized without competing depolymerization from 50 to 70 °C. The rate of polymerization (R_p) for MMBL followed the kinetic expression R_p = [AIBN]^0.54[MMBL]^1.04. The overall activation energy was calculated to be 86.9 kJ/mol, k_p/k_t^1/2 was equal to 0.050 (where k_p is the rate constant for propagation and k_t is the rate constant for termination), and the rate of initiation was 2.17 × 10^?8 mol L^?1 s^?1. The free energy of activation, the activation enthalpy, and the activation entropy were 106.0, 84.1, and 0.0658 kJ mol^?1, respectively, for homopolymerization. The initiation efficiency was approximately 1. Styrene and MMBL were copolymerized in DMF solutions at 60 °C with AIBN as the initiator. The reactivity ratios (r₁ = 0.22 and r₂ = 0.73) for this copolymerization were calculated with the Kelen–Tudos method. The general reactivity parameter Q and the polarity parameter e for MMBL were calculated to be 1.54 and 0.55, respectively. © 2003 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 1759–1777, 2003     

Kinetics of cotelomerization of 3-(trimethoxysilyl)propyl methacrylate and perfluorodecylacrylate

The telomerization of 3-(trimethoxysilyl)propyl methacrylate (TMSPMA) in the presence of 2-mercaptoethanol was investigated at 80 °C in acetonitrile. In our case, the efficiency of 2-mercaptoethanol as telogen agent, with TMSPMA, was demonstrated and the transfer constant (C_T) was determined. Moreover, cotelomerization of TMSPMA with perfluorodecylacrylate (PFDA) using various PFDA contents was investigated in order to obtain α-hydroxy oligomers with statistical copolymer-type main chains bearing trimethoxysilyl and perfluoro pendant chains. Until 10 mol% PFDA, no phase separation occured. In this composition, r_TMSPMA and r_PFDA reactivity ratios were calculated, thus showing a tendency for a statistical distribution of the monomer units in the copolymer.